Method and apparatus for production of high meat content pet foods

ABSTRACT

High meat content extruded pet feeds and methods of preparation thereof, make use of relatively high meat contents which include quantities of previously dewatered meat. In an embodiment, the total meat content of the feeds consists essentially of dewatered emulsified poultry meat or other meat sources commonly used in the pet food industry. In the methods, mixtures containing starch, fat, and meat, the latter including dewatered meat, are passed through an extruder followed by staged drying. The extruder may be of twin screw design having hollow core screws permitting introduction of steam or other heat exchange media into the screws.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims the benefit of provisional application Ser.62/645,301 filed Mar. 20, 2018, and is a continuation-in-part of U.S.application Ser. No. 15/840,926 filed Dec. 13, 2017, and is acontinuation-in-part of U.S. application Ser. No. 15/699,642 filed Sep.8, 2017, all of which are incorporated by reference herein in theirentireties.

BACKGROUND OF THE INVENTION Field of the Invention

The present invention is broadly concerned with high-meat contentextruded animal feeds such as pet feed products, having meat contentssignificantly higher than many prior art feeds. More particularly, theinvention is concerned with such feeds, as well as methods of preparingthe feeds, which preferably involve first dewatering conventional meatemulsions to produce low-moisture dewatered meat cakes, followed byextrusion of feed mixtures containing the meat cakes using a twin-screwhollow-core extruder permitting introduction of heat exchange media intothe interior of the screws. In this fashion, the moisture content of theextrusion mixtures is maintained at a level permitting satisfactoryextrusion, with sufficient inputs of specific mechanical energy andspecific thermal energy to create acceptable extruded products.

Description of the Prior Art

Manufacturers of high-end pet feeds (especially dog feeds) desire toincorporate as much meat into their extruded products as possible. Petowners increasingly favor high natural meat feeds, and such productscommand a premium price in the marketplace. These extruded feeds alsotypically include starch sources, minor ingredients such as vitamins andminerals, and a fiber source. Unfortunately, the meat source used,typically mechanically separated chicken or MSC, is a high moisturesource (around 70% moisture); this, in turn, means that only relativelysmall amounts of MSC can be directly used, because in order tosuccessfully extrude pet feeds, the total moisture content of theextrusion mixture usually cannot exceed around 48%, preferably no morethan about 43%. Above these moisture levels, it is difficult orimpossible to produce extruded feeds of acceptable quality. Hence,present-day meat-supplemented extruded pet feeds have a maximum meatcontent of around 40% by weight, based upon the total weight of the feedproducts taken as 100% by weight.

Prior art references dealing with meat-supplemented pet feeds includeU.S. Pat. Nos. 4,040,768, 6,238,726, and 6,609,819; US PatentPublications Nos. 2012/0237642, 2016/0219904, and 2017/0013848; ForeignPatent Nos. CN105559118A, CN106418615A, CN205528350U, and CN206724651U;and Wenger Manufacturing PowerPoint Presentation entitled “Pet FoodExtrusion.”

SUMMARY OF THE INVENTION

The present invention overcomes the problems outlined above and providesextruded animal feed products comprising individual quantities ofstarch, fat, and meat, with the total meat content of the productsincluding amounts of dewatered meat having a moisture content of fromabout 45-60% by weight, based upon the total weight of the dewateredmeat taken as 100% by weight. In general, the total meat contents of theproducts are greater than about 40% by weight, and more preferably fromabout 40-60% by weight, based upon the total weights of the extrudedproducts taken as 100% by weight. In turn, the total meat contents ofthe products should have dewatered meat amount of greater than 50% byweight, more preferably from about 50-100% by weight, based upon thetotal weights of the meat contents taken as 100% by weight. Mostpreferably, the meat contents of the products consist essentially of thedewatered meat.

In those instances where the total meat contents of the feeds includeunprocessed meat emulsions or meat slurries, these should be present ata level of from about 1-50% by weight, based upon the total weight ofthe meat contents taken as 100% by weight. The unprocessed meat emulsionfractions in such cases are preferably emulsified poultry meats but canbe any meat source commonly used in the industry.

The invention also provides methods for making an animal feed productcomprising the steps of passing a mixture containing individualquantities of starch, fat, and meat into and through an extruder, andprocessing the mixture by extrusion through a restricted orifice die tocreate an extrudate; the meat contents of the final products are thosediscussed above.

The dewatered meat fractions of the extruded products are preferablyprepared by passing a meat emulsion through a pair of counter-rotating,tapered, helically flighted, intermeshed screws. This dewatered meat isthen directly used with the other recipe components and fed to atwin-screw extruder. The latter includes a pair of helically flighted,intermeshed, hollow core screws, and the method includes the step ofdirecting a heating medium into the interior of the hollow core screws.The extrusion method is usually carried out without injection ofmoisture into the confines of the extruder.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a perspective view of a meat dewatering assembly in accordancewith the invention;

FIG. 2 is another perspective view of the meat dewatering assembly, froma different viewing angle;

FIG. 3 is a side elevational view of the meat dewatering assembly;

FIG. 4 is a plan view of the meat dewatering assembly;

FIG. 5 is a top view of the meat dewatering assembly, with the screwhousing removed to illustrate the configuration of the dual dewateringscrews;

FIG. 6 is a perspective exploded view of the meat dewatering assembly,illustrating alternate housing assemblies and the endmost screw supportframe in its open position;

FIG. 7 is a sectional view illustrating the forward ends of theintermeshed screws of the meat dewatering assembly, illustrating the nipclearances between the flightings of the screws;

FIG. 8 is an enlarged top view illustrating one of theU-joint/adjustment collars forming a part of the meat dewateringassembly;

FIG. 9 is a perspective view of one of the U-joint/adjustment collarsforming a part of the meat dewatering assembly;

FIG. 10 is an exploded view of one of the U-joint/adjustment collarsforming a part of the meat dewatering assembly;

FIG. 11 is a fragmentary view illustrating the water expression slots inthe housing of the meat dewatering assembly;

FIG. 12 is an enlarged view similar to that of FIG. 6, but illustratingin detail the swing frame screw support of the meat dewatering assembly;

FIG. 13 is an exploded view of a modified housing employed in anotherembodiment of the invention and equipped with a first-section steamheater; and

FIG. 14 is a fragmentary perspective view of the third housing sectionof the embodiment of FIG. 13, illustrating the pattern of drainage slotsonly on the bottom 180° of the housing section.

FIG. 15 is a perspective view of a twin-screw processing device inaccordance with the invention;

FIG. 16 is a fragmentary view of the twin-screw assembly forming a partof the device of FIG. 15;

FIG. 17 is a fragmentary view with parts broken away of the forwardoutlet end of the device of FIG. 15, depicting the reverse flightsections of the twin screws;

FIG. 18 is a partial vertical section taken along line 18-18 of FIG. 19,illustrating the internal construction of the processing device;

FIG. 19 is a vertical sectional view taken along line 19-19 of FIG. 18;

FIG. 20 is a fragmentary view with parts broken away of the forward endof another twin-screw processing device in accordance with theinvention, depicting the reverse flight sections of the twin screws;

FIG. 21 is a fragmentary view of the twin-screw assembly forming a partof the device of FIG. 20;

FIG. 22 is a sectional view of the device of FIG. 20, illustrating thefull configuration of the twin-screw assembly thereof;

FIG. 23 is a vertical sectional view taken along line 23-23 of FIG. 22;

FIG. 24 is a partial sectional view illustrating the hollow shaft/hollowhelix construction of the twin screws of the device of FIG. 15;

FIG. 25 is a fragmentary, perspective, exploded view illustrating thedrive connection and steam diffuser forming a part of the twin-screwassembly of the FIG. 20 embodiment;

FIG. 26 is a perspective view of another hollow core screw embodiment inaccordance with the invention;

FIG. 27 is a fragmentary elevational view of the screw of FIG. 26;

FIG. 28 is a fragmentary, vertical sectional view of the screw of FIG.26, illustrating the internal construction thereof;

FIG. 29 is a fragmentary, enlarged cross-sectional view of the screw ofFIG. 26;

FIG. 30 is another fragmentary, enlarged cross-sectional view of thescrew of FIG. 26;

FIG. 31 is a vertical sectional view taken along the line 31-31 of FIG.28;

FIG. 32 is a vertical sectional view taken along the line 32-32 of FIG.28; and

FIG. 33 is a schematic view illustrating a processing system inaccordance with the invention for the production of high-meat contentpet foods.

While the drawings do not necessarily provide exact dimensions ortolerances for the illustrated components or structures, FIGS. 1-32 areto scale with respect to the relationships between the components of thestructures illustrated therein.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT The Meat DewateringAssembly

Turning first to FIGS. 1-4, a meat dewatering assembly 10 is depicted,which generally includes an elongated bottom support frame 12, atwin-screw dewatering unit 14, a drive assembly 16 operably coupled withunit 14, an endmost, swingable screw support 18, and a water collectiontrough 20. As illustrated, the frame 12 supports all of the foregoingcomponents in an in-line manner, from right to left, as viewed in FIGS.1, 3, and 4.

In more detail, the support frame 12 has elongated, laterally spacedapart side members 22, 24, with intermediate connection structure 26 andspanning walls 27 extending between and interconnecting the sidemembers. The drive assembly 16 includes an electric drive motor 28having an output shaft 30 leading to gearbox 32. The gearbox 32 has apair of output shaft assemblies 34, 36, each including a firstadjustment collar 38, a first interconnected U-joint 40, a short outputshaft 42 from the first U-joint 40 to a second U-joint 44, and a secondadjustable collar 46.

The dewatering unit 14 includes a pair of uniformly tapered,non-parallel, intermeshed, helically flighted screws 52 and 54 eachhaving a central flighted region 55, rearwardly extending drive section56 extending into and supported within bearing housing 50, and forwardlyextending stub shafts 58. As illustrated, the drive section 56 extendsthrough the bearing housing 50 and is secured to adjustable collar 46.In the illustrated embodiment, the center lines of the screws 52, 54have an included angle of 2° therebetween; more broadly, this anglewould be from about 1-7°, more preferably from about 1-5°. Greaterincluded angles of 10° or more would tend to degrade the performance ofthe assembly 10 by creating unduly high nip pressure conditions at thenip regions between the screws. The regions 55 of the screws 52, 54 areof single flight design, with a uniformly decreasing pitch length fromrear to front, and a uniformly varying flight depth from rear to front.The screw 52 is a left-hand lead, variable lead (from 3.937 in. at therear end to 2.520 in. at the forward end), variable depth screw, whereasthe screw 54 is a right-hand lead, variable pitch, variable depth screwhaving the same lead dimensions. Pinch points or nip clearances 59 areprovided between the intermeshed flights along the length of the screws,which are adjustable in length. Importantly, the screws are designed andpowered to rotate in a counter-rotating fashion, i.e., they rotate inopposite clock directions.

The nip clearances 59 between the intermeshed flighting of the screws52, 54 (see FIG. 7) can be varied using the adjustment structuredescribed below between 0 and 0.161 inches at the large diameter ends ofthe screws, and from 0 to 0.086 inches at the small diameter ends of thescrews. In alternate designs, multiple helix screws may be used in lieuof the screws 52, 54, or the screws could be of constant lead orconstant pitch.

The overall unit 14 also includes a perforated, open-ended housingassembly 60, which receives the screws 52, 54, with the drive section 56extending rearwardly from the housing, and the stub shafts 58 extendingforwardly therefrom. As best seen in FIG. 6, the housing assembly 60 ismade up of three end-to-end interconnected and tapered sections 62, 64,66, with each having an internal bore 68, 70, 72 of somewhat “figure-8”configuration so as to closely surround the intercalated screws 52, 54,i.e., the housing presents two elongated, side-by-side, communicatingchambers, each surrounding and receiving a corresponding screw 52 or 54.The rearmost housing section 62 is equipped with a tubular meat inlet74. The sections 62-66 have a series of elongated, water drainage slots76 formed therein. In this embodiment, the slots 76 in section 62 are 1mm in width and 9 mm in length; the slots 76 in the downstream sections64 and 66 are smaller, with the slots of section 64 greater than thoseof section 66. Also, in the embodiments of FIGS. 1-12, the slots 76 areprovided about the entirety of the housing 60 and along the full lengththereof. As best seen in FIGS. 1 and 3, a series of upright mounts 78are secured to the side members 22, 24, and extend upwardly forconnection to the housing sections, thereby suspending the housing 60above the support frame 12. The open housing design ensures that themeat dewatering operation of the assembly 10 occurs at substantiallyatmospheric pressures in contrast to typical extruders which normallyoperate at superatmospheric pressures.

As depicted in FIG. 6, use may be made of an alternate housing assembly60 a, which is identical to the assembly 60 except that the bores 68 a,70 a, and 72 a have essentially flat intermediate sections and roundedends. Consequently, the walls of the housing sections 62 a, 64 a, and 66a do not closely conform to the configuration of the screws 52, 54 atthe intermeshed regions thereof.

The swingable screw support 18 is mounted to the forward end of supportframe 12 by means of a pivot assembly 80, allowing the support 18 to beselectively moved from a closed position, illustrated in FIGS. 1-5, toan open position, illustrated in FIG. 6. Appropriate latching structure(see FIGS. 6 and 12) is provided to hold the support 18 in its closedposition, with an attach/detach crank 82. When it is desired to open thesupport, the crank 82 is actuated, and the support is swung outwardly tothe FIG. 6 position. The support 18 is provided with a fixture 84 havinga pair of side-by-side bearing supports 86, which receive the forwardlyprojecting stub shafts 58 of the screw 52, 54; thus, the screws aresupported at both ends thereof during operation of the assembly 10.

The water collection trough 20 positioned under housing 60 is ofgenerally U-shaped configuration and is designed to receive waterexpressed through the housing slots 76. Suitable water take-awaystructure (not shown) is provided for draining of the trough 20 duringoperation of the assembly 10.

As indicated previously, the nip clearances between the screws 52, 54can be varied. In order to do this, use is made of one or more of theadjustment collars 38. Referring to FIGS. 8-10, the adjustmentcollar/U-joint 46/44 is illustrated. Specifically, the rearmost end ofdrive section 56 of screw 54 is secured to the collar 46. The collar 46has a first radially expanded segment 88 having a pair of opposed lugs90. The collar 46 also has a second segment 92 having a pair of opposedlug-receiving recesses 94. The segment 92 is secured to U-joint 44 bymeans of screws 96. The recesses 94 are defined by a pair of projections98, each carrying an adjustment screw 100; the screws 100 engage thelugs 90 as shown. When it is desired to change the relative position ofthe screw 54 relative to the screw 52, and thereby change the nipclearances therebetween, it is only necessary to turn one of theadjustment screws 100, which affects a slight rotation of the collar 46,and thereby the entirety of the screw 54. Of course, such adjustmentscan only be made when the assembly 10 is not in operation.

FIG. 13 illustrates a modified embodiment in the form of a meatdewatering assembly 102. In this embodiment, a screw assembly housing104 is provided made up of first, second, and third end-to-endinterconnected housing sections 106, 108, and 110. The initial housingsection 106 is equipped with a surrounding steam-heating jacket 112,which serves to heat the emulsified meat introduced through the inlet114. Moreover, in this embodiment, the intermediate housing section 108is equipped with water-drainage slots 76, which cover the full surfacearea of the section 108. The final section 110 has slots 76 only on thebottom half thereof, as best seen in FIG. 14.

It is desirable that meat to be processed in the assembly 10 be firstmechanically conditioned into an emulsified form, which may beoptionally preheated to a temperature of from about 40-80° C., beforedelivery to the inlet 74. The meat then passes along the length of thehousing 60 during counter-rotation of the screws 52, 54, the latterpowered by means of drive assembly 16. As the meat traverses the lengthof the housing at substantially atmospheric pressures, the intermeshedscrews serve to press or squeeze the meat particles within theemulsified meat, to thereby expel water through the housing slots 76 forcollection within and take-away from trough 20. The fully dewatered meatthen passes through the open forward end of the housing 60 where it iscollected, by a suitable conveyor or other apparatus (not shown)separately from the expressed water. In normal practice, the screws 52,54 are counter-rotated at a speed of from about 30-200 rpm, morepreferably 50-150 rpm, which differs from typical twin-screw extrudersequipped with high rotational speed, co-rotating screws.

The Hollow Core Screw Extruder

Turning now to the drawings, and particularly FIGS. 15-19, a processingdevice 220 is illustrated. Broadly speaking, the device 220 includes anelongated, tubular barrel 222 having a material inlet 224 and an opposedprocessed material outlet 226, with a twin-screw assembly 228 within thebarrel 222.

As illustrated, the barrel is made up of a plurality of end-to-endinterconnected barrel sections 230, 232, 234, and 236. An internal linerassembly 238 is located within and extends along the length of thesections 230-236 and presents a pair of elongated, juxtaposedcommunicating arcuate passageways 240, 242, which receive the twin-screwassembly 228. The sleeve further presents the rearmost opening 244, asbest seen in FIG. 18. An apertured front wall 246 is located at theopposite end of the barrel and is secured thereto. Additionally, aforwardly projecting bearing housing 2 48 is attached to the outer faceof front wall 246, and has a pair of side-by-side tubular bearingstherein.

The twin-screw assembly 228 includes identical, complemental first andsecond intermeshing, double-flight screws 250 and 252, which aredesigned to directionally co-rotate during the operation of device 220.Referring to FIGS. 16 and 18, it will be seen that the screws 250, 252each have an elongated shaft 254 with outwardly extending, helicalfighting 256 along the length of the shaft 254, having a pitch length of1, based upon the screw diameter. An elongated central bore 258 extendssubstantially throughout the length of the shaft 254, thereby creating ahollow core 260 therein. As best seen in FIG. 17, the fighting 256 isdivided into two sections, namely a first section 262 operable to conveymaterial from the inlet 224 toward and through the processed materialoutlet 226, and a second section 264 operable to retard the flow ofmaterial therepast. To this end, the flighting sections 262, 264 are ofreverse hand, respectively. The rearmost ends of the screws 250, 252 areprovided with drive and bearing structure 266, 268, having rearmost,splined connector ends 270, 272; the ends 270, 272 are designed to matewith suitable drive structure (not shown) for axially rotating thescrews. The forward ends of the screws are equipped with elongatedextensions 274, 276, which are received within the tubular bearings ofhousing 248 (FIG. 17).

The screws 250, 252 are equipped with structure 278 to supply heatexchange media to the internal cores thereof. Specifically, elongated,stationary steam delivery tubes 280 and 282 extend from a point outsideof housing 222 adjacent front wall 246 and into the bores 258. The tubes280, 282 extend through the endmost tubular fixtures 284, 286 located atthe forward ends of the extensions 274, 276. The outermost ends of thetubes 280, 282 connect with identical rotary unions 288, 290. Each suchunion includes a block 292 having a media inlet opening 294, a liquidremoval outlet 296, and a rotatable sleeve 298 disposed about thecorresponding tube 280 or 282. To this end, the sleeves 298 are securedto the corresponding tubular fixtures 284, 286.

The screws 250, 252 are preferably fabricated from metal using normalmachining techniques and are normally case-hardened.

In operation, material to be processed (which may be preconditioned, asexplained hereafter) is delivered to inlet 224 during co-rotation of thescrews 250, 252, which serves to advance the material during processingthereof to deliver processed material to outlet 226. During thisoperation, heat exchange media (normally steam) is directed from adelivery conduit (not shown) coupled with the media inlets 294 and intothe tubes 280, 282 to the open cores 260 of the screws in order toprovide thermal energy required for processing of the material.Additional energy input is provided by means of pressure and shearconditions developed within the barrel 222. During processing, steamcondensate passes from the cores 260 and through the sleeves 298,exiting the system via the removal outlets 296. In order to preventleakage of material past the wall 246 and the fixtures 284, 286, thereverse flight section 264 comes into play by creating a retardationforce against the flow of material created by the opposite hand fightingof the section 262. The product emerging from the outlet 226 may then bepassed through a restricted orifice extrusion die and cut, in order toform the final product, although in practice, the elongated deliverypipe is normally secured to the outlet 226 and a final die and knifeassembly are located at the opposite end of the pipe.

FIGS. 20-25 illustrate another embodiment of the invention, in the formof a processing device 300. The device 300 is in many respects similarto the device 220, having a tubular barrel 302 with a twin-screwassembly 304 therein, and having an inlet 224 and an outlet 226, as inthe case of the first embodiment. Again, the barrel 302 is made up oftubular, interconnected barrel sections 306-312 with an internal linerassembly 314 defining side-by-side passageways 316, 318. The forward endof barrel 302 is equipped with a front wall 320, which supports aforwardly projecting bearing housing 322.

The screw assembly 304 has a pair of identical, intermeshed, singleflight, helical screws 324, 326, which are received within thepassageways 316, 318. Each of the screws has an elongated central shaft328, 330, as well as outwardly extending helical flighting 332, 334along the length thereof. As in the case of the first embodiment, thescrews 324, 326 have rearmost drive and bearing structures 336, 338,equipped with splined drive connection ends 340, 342. The forward endsof the screws have bearing extensions 344, 346, which are receivedwithin the bearings of housing 322.

The principal differences between the first and second embodiments arethe configuration of the helical screws 324 and 326. Specifically, eachsuch screw includes a primary central section 348 operable to moveproduct along the length of the barrel 302 towards and through theoutlet 226, an inlet section 350 operable to deliver incoming materialto the section 348, and a forward, material flow retarding section 352.The inlet section 350 is advantageously a machined part having a centralshaft 354 with an internally splined bore 356, and outwardly extendingfighting 332, 334. As best seen in FIG. 24, the bore 356 is designed toreceive the forward end of the corresponding drive and bearing structure336, 338. The screw sections 348 and 350 have a pitch length of 1, basedupon the screw diameter, and denoted by D1 of FIG. 24. The forwardsection 352 of each screw is likewise a machined part and has a central,bored shaft 360 with outwardly extending helical flighting 362. Notably,the pitch of the flight 362 is opposite that of the pitch of theflighting 358 of screw section 348, and has a pitch length of 0.3, basedupon the screw diameter, denoted by D2 of FIG. 24. Preferably, the pitchlength D1 should be from about 0.4-1.2, more preferably 0.5-1.0, whereasthe pitch length D2 should be from about 0.2-1.1, more preferably 0.3-1.

The central section 348 is preferably formed by casting (e.g., sand orinvestment casting) with a plurality of sections which are butt-weldedtogether to form the entirety of the central section. As best seen inFIG. 24, the central section 348 has a central shaft 366, which ishollow along the length thereof to define a central core 367, as well asoutwardly extending flighting 368, which is likewise hollow to define ahelical core 369. In this regard, the flight 368 is defined by outwardlyextending, opposed, spaced apart sidewalls 370 and 372, with a flattenedouter wall 374. As such, it will be observed that there is a helicaltransition 376 between the innermost ends of the sidewalls 370, 372,which provides full, open communication between the central core 367 andthe helical core 369, without any blockage or narrowing whatsoever;stated otherwise, the transition 376 presents an area which is openthroughout the length and width thereof in order to afford unobstructedcommunication between the hollow regions of the shaft and helical screw.Inasmuch as the section 348 is of cast construction, it will be seenthat the thickness of the shaft 366 is essentially identical with thethicknesses of the sidewalls 370, 372, and outer wall 374.

In preferred forms, the length of the central screw section 348 is atleast about three times, more preferably at least about five times,greater than the length of the forward screw section 352.

The screws 324, 326 receive elongated media delivery tubes 378, 380,which are designed to deliver media such as steam to the interior of thescrew sections 348 and 352. The forward ends of the tubes 378, 380 arereceived within rotary unions 288, 290, identical to those described inconnection with the first embodiment, and like reference numerals havebeen applied (FIG. 24). The rotatable sleeves 298 are supported bycouplers 284, again as described in the first embodiment.

The innermost ends of the tubes 378, 380 are each supported by atubular, open-sided diffusion cage 382. The latter includes a mountingscrew 384, which extends through the end of the primary screw section348 and is received within a threaded bore 386 in the forward butt endof bearing and drive structure 336.

The rearmost end of the screw section 348 has a splined portion 388,which receives the forward end of the structure 336 ahead of inlet screwsection 350. The forward end of the screw section 348 is secured to therearward end of screw section 352 by butt welding or any otherappropriate technique. Hence, driving rotation of the structures 336serves to rotate the entire screws 324, 326.

The operation of device 300 is similar to the device 220. However, owingto the completely open hollow core structure of the screw section 348,better heat transfer from the injected steam is afforded, as comparedwith the device 220.

FIGS. 26-32 illustrate another hollow core screw embodiment of theinvention in the form of helical extrusion screw 390. The screw 390 isdesigned for use in a twin-screw extruder so that a mating screw (notshown) will be used in conjunction with the screw 390 to make a screwset. Generally, the screw 390 includes an elongated central shaft 392with a continuous helical fighting 394 along the length thereof.

The shaft 392 has a rearmost splined section 396 to afford a drivingconnection with a motor/gear reducer assembly and a forward bearingextension. The shaft 392 is a machined, case-hardened part and has asolid rear section 398 and a hollow core forward section 400 presentingan elongated, axially extending, central core 402. The forward end ofthe core 402 is equipped with a coupler 404 designed to receive a rotaryunion 288 (FIG. 28). A stationary steam delivery tube 408 (shownfragmentarily in FIG. 28) extends substantially the full length of thecore 402 and has an open end 410.

The fighting 394 includes a rear section 412 of relatively narrow flightwidth, which extends the full length of the solid section 398.Additionally, the fighting 394 has a wider flight width forward section414 presenting an outermost flight surface 414 a, which extends from theend of section 412 to a point close to the forward end of the shaft 392.However, as in the case of the earlier embodiments, the screw 390 has areverse flight section 416 between the end of section 414 and coupler404.

In the manufacture of the screw 390, the fighting 394 is machined as asolid protrusion from the shaft 392, with a continuous, helical,open-top groove 418 in the wide flight section 414, extending from theoutermost flight surface 414 a inwardly to an inner wall 420 close tothe core 402. Thereafter, a series of spaced apart apertures 422 areformed along the length of the inner wall 420, in order to communicatethe core 402 with groove 418. Next, a helical cover piece 424 ispositioned over the upper end of the groove 418, and is welded to thefighting section 414. In the final step, the screw 390 is machined toprovide the proper outside diameter for the flighting 394. This createsa unitary construction, as illustrated in the drawings.

The operation of the screw 390, with its mating, intermeshed screwwithin an extruder barrel, such as barrel 222, is the same as describedin connection with the embodiment of FIGS. 15-19. That is, co-rotationof the screw set serves to advance material during processing thereoffrom the barrel inlet to the barrel outlet. Simultaneously, steam orother heat exchange media is directed into the core 402 through theunion 288 and the extension of shaft 392 beyond the end of the extruderbarrel. This media flows through the core 402 and groove 418 owing tothe communicating apertures 422. This provides an increased level ofthermal energy to the process. The reverse flight section 416 alsoserves to retard the flow of material at the forward end of the screw390.

FIG. 33 schematically illustrates a system 426 for the production ofhigh-meat content pet foods, and broadly includes an upstream meatdewatering assembly 10 operably coupled with an extrusion systemgenerally having an optional preconditioner 428, an extruder 430, and apost-extrusion terminal assembly 440 including a drying assembly 446.The extruder 430 is a modified version of the devices 220 or 300, usingany of the hollow core screws described above. The extruder 430 includesa generally L-shaped conduit or pipe 432 affixed to barrel outlet 226and extending to the terminal assembly 440. The use of pipe 432 permitsattachment of steam lines to the previously described rotary unions 288,290 (FIG. 20).

The meat dewatering assembly is designed to treat high-moisture meatproducts, such as emulsified poultry (e.g., chicken or turkey) productsto substantially reduce the moisture levels thereof and createlow-moisture meat cakes. Such emulsified products typically contain fromabout 60-80% by weight moisture, and treatment in the assembly 10 servesto reduce the moisture content such that the final meat cakes usuallyhave a moisture content of from about 45-60% by weight, more preferablyfrom about 48-55% by weight, based upon the total weight of thedewatered meat taken as 100% by weight.

The system 426 in further detail includes a conveyor 434 and dewateredmeat cake delivery line 436 leading to the input 224 of the extruder430. In some cases, it may be desirable to use emulsified meat alongwith dewatered meat cake and, to this end, an optional emulsified meatinlet line 438 is provided, which leads to extruder input 224. Ifdesired, the preconditioner 428 may be used, and in such a case the meatinlet lines 436 a, 438 a would direct the meat products through thepreconditioner 428 before entering the extruder inlet 224. In preferredpractice, the preconditioner 428 is operated without any injection ofmoisture by way of steam or water, and thus the preconditioner wouldprincipally serve as a means of uniformly mixing the ingredients to beprocessed in the extruder 430.

As noted, the output end of pipe 432 is operably coupled to a terminalassembly 440 made up of an adjustable back pressure valve 442 and anextrudate hood 444, with a restricted orifice die (not shown) located atthe entrance to the hood 444. These components are fully illustrated anddescribed in U.S. Pat. No. 9,320,298, which is incorporated by referenceherein in its entirety. The valve 442 is designed to provide a selectivedegree of restriction of flow of material from pipe 432 as the materialpasses through the endmost die. The extrudate hood 444 serves tofacilitate the spread of extrudate issuing from the die to preventagglomeration or clumping of the extrudate. The hood 444 includes ashiftable conveyor belt (not shown), in order to move the product fromthe die area to the hood exit.

The dryer assembly 446 is made up of a relatively short pre-dryer 448and a final dryer 450 of conventional design. In some instances, it hasbeen found that high-meat extrudates issuing from the die are delicateand prone to fragmentation. Accordingly, in these case, the extrudatefrom the hood 444 passes immediately into the pre-dryer, which serves to“set” the products and preserve the integrity thereof, prior to passageto the final dryer.

The system 426 is designed to produce extruded products using mixturesof meat including dewatered meat, with the optional presence offull-moisture meat or meat emulsion, together with other conventionalpet food ingredients such as grains, starches, and fats, with optionalminor ingredients such as vitamins and emulsifiers.

In general, the products should contain from about 5-50% by weightstarch, from about 3-12% by weight fat, and a preferred moisture contentof from about 6-12% by weight, all of the foregoing percentages basedupon the total weight of the product taken as 100% by weight.

The total meat content can consist essentially of dewatered meat, or amixture of such dewatered meat with whole meat and/or meat emulsion(s).Where the total meat content is made up of a combination of dewateredmeat and other meat sources such as emulsified meat, the dewatered meatshould be present at a level of from about 50-100% by weight, morepreferably from about 85-100% by weight, based upon the total weight ofthe meat content taken as 100% by weight; correspondingly, the meatemulsion, if used, should be present at a level of from about 0-50% byweight, more preferably from about 1-15% by weight, again based upon thetotal weight of the meat content taken as 100% by weight.

Advantageously, the total meat content of the products consistsessentially of dewatered meat, because adding untreated meat or meatslurry emulsions increases the moisture content of the mixture to beextruded, which is to be avoided.

In all cases, whether the total meat content is made up entirely ofdewatered meat or a combination of dewatered meat and untreated meatemulsion and/or meat slurry, it is important to understand the basis fordetermining the meat content of the products. For example, (1) the totalmeat content may be expressed as a percentage of the dry recipecomponents, i.e., the dry components are taken as 100% by weight; or (2)the total meat content may be expressed as a percentage of the totalrecipe, i.e., the total recipe including the total meat content is takenas 100% by weight; or (3), similar to (1), the total meat content may beexpressed as an equivalent meat slurry level, i.e., as if the total meatcontent were present as meat slurry, with the meat slurry levelexpressed as a percentage of the total dry recipe components; or (4),similar to (2), the equivalent meat slurry level may be expressed as apercentage of the total recipe components taken as 100% by weight. Froma commercial perspective, current labeling laws and regulations allowthe pet food manufacturer to advantageously express the meat content asin (4).

The following Table 1 sets forth approximate broad and preferred rangesin the case where the meat content is entirely in the form of dewateredmeat and expresses those ranges as set forth in (1)-(4) above. It shouldbe understood in this respect that the data in columns (3) and (4) are,correspondingly, the values of columns (1) and (2) multiplied by 3.33;this reflects the fact that each pound of dewatered meat was made from3.33 pounds of starting meat slurry. Moreover, the values of column (2)are equal to the values of column (1) divided by the values of column(1) plus 100, and the values of column (4) are equal to the values ofcolumn (3) divided by the values of column (3) plus 100.

TABLE 1 (1) (2) (3) (4) Dewatered meat Dewatered meat Equivalent meatEquivalent meat expressed as expressed as slurry level slurry level % ofthe % of the expressed as % expressed as % of dry recipe total recipe ofdry recipe the total recipe Process Range components componentscomponents components Broad range 85.0-120.0 46.0-54.5 156.0-400.060.9-80.0 Preferred range 85.0-105.0 46.0-51.2 156.0-350.0 60.9-77.8

The above Table 1 represents preferred implementations of the inventionwherein the total meat content is in the form of dewatered meat. If thetotal meat content includes untreated meat emulsion or meat slurry, suchwill normally reduce the total meat content which can be employed in theproducts, inasmuch as meat or meat slurry will have a greater moisturecontent than the dewatered meat. As noted above, the total moisturecontent of the mixture fed to the extruder is important, in order topermit proper extrusion processing of the mixture. Typically, thismoisture content should be from about 25-48% by weight, more preferablyfrom about 35-43% by weight, based upon the total weight of the mixturefed to the extruder taken as 100% by weight.

During extrusion processing, the ingredients passing through theextruder should be heated to a minimum temperature of 70° C., or morepreferably ≥90° C., in order to meet feed safety requirements. Therotation of the extruder twin screws should be in the range from about100-600 rpm, more preferably from about 300-450 rpm; pressure within theextruder barrel is normally from about 200-600 psi, more preferably fromabout 300-400 psi. Pressurized steam is directed into the hollow corescrews usually at a level of 30-120 psi, more preferably from about45-90 psi, depending upon the size of the extruder. Although notillustrated in the drawings, it is possible to employ extruder barrelswhich are externally jacketed for receiving steam or other heat exchangemedia in order to indirectly heat the materials passing through theextruder. The jacket steam would likewise be pressurized to a level ofabout 30-120 psi, more preferably from about 45-90 psi.

In the drying assembly 446, the pre-dryer 448 is of multiple-pass designand employs heated air at a temperature of from about 100-240° C., morepreferably from about 140-180° C., with a total retention time of fromabout 3-12 minutes, more preferably from about 5-10 minutes. The finaldryer 450 is likewise of multiple pass design and employs heated airhaving a temperature less than that utilized in the pre-dryer, namelyfrom about 70-140° C., more preferably from about 85-110° C., with atotal residence time of from about 6-20 minutes, more preferably fromabout 8-15 minutes.

The optional preconditioner 428 may take a variety of forms, so long asthe starting mixtures are substantially uniformly mixed prior todelivery to the inlet 224; it is also possible to add moisture duringpreconditioning, but this is normally minimized or eliminated, owing tothe high moisture content of the meat fraction of the mixtures. Forexample, commercially available Wenger DDC or HIP preconditioners (seeU.S. Pat. Nos. 4,752,139, 7,448,795, and 9,028,133) may be used in thiscontext. Such preconditioners may provide steam and/or water injectionin order to heat and pre-cook the starting mixtures, or in someinstances hot air may be used as a heating medium (U.S. Pat. No.7,963,214). In such instances, it may be necessary to provide only aportion of the meat fraction of the mixture during passage through thepreconditioner, with separate introduction of the remainder of the meatfraction directly into the input 224 of the processing device, alongwith the preconditioned materials, to achieve the desired totalpercentage of meat.

It will be appreciated that in extrusion technology there are twoprincipal sources of energy input, referred to as specific mechanicalenergy (SME), and specific thermal energy (STE). SME is primarilyderived from the heat, friction, and shear forces developed by theextrusion screw(s), whereas STE is generated by the addition of heatexchange media, typically steam. In existing extrusion technology, STEis most commonly added by means of direct injection of steam into themixture being processed, either in the preconditioner, the extruder, orboth. However, as indicated above, direct injection of steam can beproblematical when high-meat recipes are being processed. The presentinvention provides a distinct improvement, in that indirect heating isachieved in the extruder, which avoids direct steam addition and theconsequent excess moisture problems attendant thereto.

EXAMPLE

In this example, a series of pet food runs were carried out using theapparatus of FIG. 33, with a Wenger HIP preconditioner 428, and anextruder 430 equipped with the hollow core screws illustrated in FIGS.27-32. In addition, the extruder was provided with jacketed barrel headsallowing introduction of steam for the indirect heating of the materialpassing through the extruder barrel.

In each run, a dry recipe was used made up of 26% poultry meal, 36%whole potato flour, 26% yellow pea flower, 8% beet pulp, 3% flax meal,and 1% salt, all percentages based upon the total weight of the dryrecipe taken as 100% by weight. The moisture content of the dry recipewas 8.6%. Two different meat sources were used in the runs, specificallymechanically separated chicken (MSC) in the form of a high-moistureemulsion, and dewatered MSC meat cake (having a moisture content ofabout 50% by weight) derived from initial processing of MSC using themeat dewatering assembly 10 (333 kg of MSC yields 100 kg of MSC meatcake). In general, the process involved directing the dry ingredientsand the meat sources to the preconditioner 428 for mixing therein priorto delivery to the extruder 430; however, no moisture was added duringpreconditioning. When emulsified meat was used, it was preheated to 40°C. prior to delivery to the preconditioner. Thereupon, thepreconditioned mixtures were passed through the extruder 430, and thenthrough the assemblies 440, 446 to complete the process.

In greater detail, a total of five runs were carried out, using thefollowing meat ingredients, as set forth in Table 2:

TABLE 2 MSC Dewatered Run No. MSC % Cake % 1 60 0 2 60 57.2 3 60 41 4 090 5 0 103

-   -   weight percentage based upon the total weight of the dry        ingredients in the mixture taken as 100% by weight

In carrying out the runs, the extruder heads and hollow core screws werefully heated with injected steam. In particular, the steam was injectedat a pressure of 120 psig into both the extruder heads and hollow corescrews, with the steam flow through the heads at a level of about 20-45kg/hr, with a steam flow of about 40-45 kg/hr through the hollow corescrews. It can be appreciated by those skilled in the art of extrusion,that steam flow rates can be varied depending on the size of theextruder and the throughput capacities of the extrudate.

The extrusion mixtures made up of the dry recipe and meat sources wereinitially passed through a Wenger HIP preconditioner 428 without anyinjection of steam or water into the mixtures; accordingly, thepreconditioner 428 thoroughly mixed the ingredients prior tointroduction of the mixtures into the extruder inlet. As the productemerged from the extrusion die and entered the hood 444, fan air wasblown onto the products in order to prevent them from adhering to thehood.

The following Table 3 sets forth data collected in these runs.

TABLE 3 Dry feed Meat Moisture % by wt Bulk Density (g/l) Run rate Cook% MSC cake Off Off No. (kg/hr) OE¹ kg/hr kg/hr CVR² OE¹ OD³ OE¹ CVR² OD³1 500 89.2 300 0 16.7 32.3 2.4 555 444 402 2 500 95.7 300 286 33.2 43.36.9 540 514 421 3 500 92.4 300 205 24.9 40.3 4.8 580 505 436 4 500 96.40 450 34.3 38.7 4.4 580 472 376 5 500 97.4 0 514 31.8 46.9 1.6 582 528370 ¹OE means the cook, moisture, or bulk density values of the productoff of the extruder prior to any drying thereof. ²CVR means the moistureor bulk density values of the product taken off the pre-dryer prior toany final drying thereof. ³OD means the moisture and bulk density valuesof the product after complete drying thereof.

The following Table 4 sets forth the proximate analysis of the final,dried products:

TABLE 4 Proximate analysis (% by wt) Run No. Protein Fat⁴ Moisture AshFiber 1 30.9 9.0 5.1 7.0 4.6 2 37.1 11.4 7.4 8.7 3.6 3 34.8 10.3 6.6 8.13.7 4 39.9 12.4 6.2 8.3 4.8 5 40.0 12.8 6.9 8.7 2.9 ⁴The fat level wasbased upon the extruded and dried product, before any downstream coatingthereof.

The cook values for the extruded products were all satisfactory, and theproducts after drying were of acceptable bulk density and productintegrity. That is, the products were commercially acceptable asextruded pet feeds.

We claim:
 1. An extruded animal feed product comprising individualquantities of starch, fat, and meat, the total meat content of saidproduct including an amount of dewatered meat having a moisture contentof from about 45-60% by weight, based upon the total weight of thedewatered meat taken as 100% by weight.
 2. The product of claim 1, saidtotal meat content of the product being from about 40-60% by weight,based upon the total weight of the extruded product taken as 100% byweight.
 3. The product of claim 1, said meat content of said producthaving a dewatered meat amount of from about 50-100% by weight, basedupon the total weight of the meat content taken as 100% by weight. 4.The product of claim 3, said total meat content consisting essentiallyof said dewatered meat.
 5. The product of claim 1, said total meatcontent including an amount of emulsified meat.
 6. The product of claim5, said amount of emulsified meat being from about 1-50% by weight,based upon the total weight of the meat content taken as 100% by weight.7. The product of claim 5, said emulsified meat comprising emulsifiedpoultry meat or any other meat source commonly used in the pet foodindustry.
 8. The product of claim 1, said starch being present at alevel of from about 5-50% by weight, and said fat being present at alevel of from about 3-12% by weight, all of the foregoing percentagesbased upon the total weight of the product taken as 100% by weight. 9.The product of claim 1, said product having a moisture content of fromabout 6-12% by weight.
 10. The product of claim 1, said product having abulk density of from about 22-40 lb/ft³.
 11. The product of claim 1,said product having a cook value of at least about 85%.
 12. A method ofmaking an animal feed product comprising the steps of passing a mixturecontaining individual quantities of starch, fat, and meat into andthrough an extruder, and processing said mixture by extrusion through arestricted orifice die to create an extrudate, followed by drying of theextrudate, the total meat content of said product including an amount ofdewatered meat having a moisture content of from about 45-60% by weight,based upon the total weight of the dewatered meat taken as 100% byweight.
 13. The method of claim 12, said meat content of the productbeing from about 40-60% by weight, based upon the total weight of theextruded product taken as 100% by weight.
 14. The method of claim 12,said meat content of said product having a dewatered meat amount of fromabout 50-100% by weight, based upon the total weight of the meat contenttaken as 100% by weight.
 15. The method of claim 14, said total meatcontent consisting essentially of said dewatered meat.
 16. The method ofclaim 12, said total meat content including an amount of emulsifiedmeat.
 17. The method of claim 16, said amount of emulsified meat beingfrom about 1-50% by weight, based upon the total weight of the meatcontent taken as 100% by weight.
 18. The method of claim 16 saidemulsified meat comprising emulsified poultry meat or other meat sourcescommonly used in the pet food industry.
 19. The method of claim 12, saidstarch being present at a level of from about 5-50% by weight, and saidfat being present at a level of from about 3-12% by weight, all of theforegoing percentages based upon the total weight of the product takenas 100% by weight.
 20. The method of claim 12, said product having amoisture content of from about 6-12% by weight.
 21. The method of claim12, said product having a bulk density of from about 22-40 lb/ft³. 22.The method of claim 12, said product having a cook value of at leastabout 85%.
 23. The method of claim 12, including the steps of creatingsaid dewatered meat by passing a meat emulsion through a pair ofcounter-rotating, tapered, helically flighted, intermeshed screws. 24.The method of claim 12, said extruder having a pair of helicallyflighted, intermeshed, hollow core screws, said method including thestep of directing a heating medium into the interior of said hollow corescrews.
 25. The method of claim 12, said extruder having a barrelequipped with jackets, said method further including the step ofdirecting a heating medium into said jackets.
 26. The method of claim12, including the step of carrying out said extrusion without injectionof moisture into the confines of the extruder.
 27. A product prepared inaccordance with the method of claim 12.